EP3207225B1 - Verfahren zum ausgleich von lastspitzen bei der energieerzeugung und/oder zur erzeugung von elektrischer energie und/oder zur wasserstofferzeugung - Google Patents

Verfahren zum ausgleich von lastspitzen bei der energieerzeugung und/oder zur erzeugung von elektrischer energie und/oder zur wasserstofferzeugung Download PDF

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Publication number
EP3207225B1
EP3207225B1 EP15790029.1A EP15790029A EP3207225B1 EP 3207225 B1 EP3207225 B1 EP 3207225B1 EP 15790029 A EP15790029 A EP 15790029A EP 3207225 B1 EP3207225 B1 EP 3207225B1
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EP
European Patent Office
Prior art keywords
heat storage
carrier gas
heat
storage module
gas
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EP15790029.1A
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German (de)
English (en)
French (fr)
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EP3207225A1 (de
Inventor
Klaus Knop
Robert Joseph PFAB
Lars Zoellner
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Carbon Clean Technologies GmbH
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Carbon Clean Technologies GmbH
Carbon Clean Tech AG
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/065—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle the combustion taking place in an internal combustion piston engine, e.g. a diesel engine
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K23/00—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids
    • F01K23/02—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled
    • F01K23/06—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle
    • F01K23/10—Plants characterised by more than one engine delivering power external to the plant, the engines being driven by different fluids the engine cycles being thermally coupled combustion heat from one cycle heating the fluid in another cycle with exhaust fluid of one cycle heating the fluid in another cycle
    • F01K23/101—Regulating means specially adapted therefor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
    • F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/14—Combined heat and power generation [CHP]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00—Combustion technologies with mitigation potential
    • Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
    • Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]

Definitions

  • the invention relates to a method for balancing load peaks in the generation of electrical energy and/or for the particularly decentralized generation of electrical energy, more particularly from renewable energy sources, such as biogas from biomass fermentation or synthesis gas from biomass gasification, or from fossil fuels, such as Natural gas, by using the heat from heated carrier gas to generate electricity, in particular in a thermoelectric storage power plant, and/or to use the heat from heated carrier gas to generate hydrogen, in particular in a gasification process.
  • the invention relates to a thermoelectric storage power plant.
  • a power plant that has storage facilities for thermal energy is from the US 2012/0137702 A1 known.
  • biomass is burned in a gas burner and the flue gas is then routed through a heat storage module, which stores a large part of the energy in the flue gas in the form of heat.
  • a heat storage module which stores a large part of the energy in the flue gas in the form of heat.
  • valves are actuated, whereupon the flue gas is fed to a second, empty storage module, so that the second storage module is subsequently loaded.
  • a water-air mixture is passed through the first storage module.
  • the first memory module is discharged in the process.
  • the resulting steam is expanded in a downstream turbine and the energy released can be converted into electricity.
  • the two memory modules are loaded and unloaded alternately.
  • the purpose of the storage modules is to supply the energy contained in the flue gas to the turbine without having to direct the flue gas into the turbine, which could damage the turbine.
  • a power plant with two heat storage modules is from the U.S. 7,444,818 B1 known.
  • a previously compressed gas is passed through a first heat storage module that has been previously charged and is thereby heated.
  • the gas is expanded in a first low-pressure turbine and then fed to a combustor.
  • the flue gas produced there is passed through a second heat storage module and transfers heat to it there, as a result of which the second heat storage module is loaded. Water is then added to the flue gas and the superheated steam fed to a high-pressure turbine.
  • the first memory module is discharged while the second memory module is charged. If the second heat storage module is fully loaded, valves are switched so that the first heat storage module is loaded and the second heat storage module is unloaded.
  • the heat storage modules thus ensure that the gas in front of the first turbine is preheated.
  • the object of the present invention is to provide a method and a storage power plant of the type mentioned at the outset which, with high cost-effectiveness and high efficiency, enable the balancing of generation peaks and generation troughs in the generation of electrical energy and thus make a contribution to load management in the power grid can provide, whereby energy is stored in times of high power generation and low power demand and released again at peak loads.
  • the method and storage power plant are intended to enable, in particular, decentralized power generation and/or hydrogen generation with high cost-effectiveness and high efficiency.
  • the method according to the invention enables the heat from highly heated carrier gas, in particular hot air, to be used to generate electricity in a power plant process or to generate hydrogen, in particular in a gasification process, in which case a carrier gas, such as air, is first heated to a specific loading in at least one gas heater of a storage power plant -Set temperature is heated.
  • the hot carrier gas is used for thermal loading of at least one heat storage module of a plurality of heat storage modules of the storage power plant, heat being released from the hot carrier gas from the gas heater to a heat storage material of the heat storage module (loading cycle).
  • a plurality of gas heaters can be used to generate hot gas in sufficient quantities and/or with a sufficiently high target loading temperature for loading the heat storage modules.
  • a maximum loading setpoint temperature when heating the carrier gas in the gas heater can be 1000°C to 1300°C, preferably 1100°C to 1200°C.
  • a separate gas heater can be assigned to each heat storage module.
  • the stored usable heat or the usable heat content of the heat storage module is used to heat cold carrier gas, in particular cold air, with cold carrier gas flowing through at least one heat storage module and heat is transferred from the heat storage material to the carrier gas (discharge cycle).
  • the carrier gas is heated to a specific discharge temperature as it flows through the heat storage module and exits the heat storage module at this temperature level.
  • the target discharge temperature required for heat utilization can be at least 500° C., preferably at least 600° C., up to 900° C., more preferably up to 800° C.
  • the heat of the hot carrier gas generated during a discharge cycle is then used in a power plant or gasification process.
  • Both the charging cycle and the discharging cycle can be associated with a partial or complete charging or discharging of a heat storage module.
  • the usable heat content of a heat storage module results from the specific heat capacity of the heat storage material, the mass of the heat storage material or the size of the heat storage module and the (average) heat storage temperature that is reached during a charging or discharging cycle or process.
  • heat from carrier gas heated in at least one heat storage module is transferred to a working fluid of the power plant process, in particular to a working fluid of a steam power process.
  • the working fluid is preferably water.
  • the heat transferred to the carrier gas can be used in a conventional steam power plant, the power class of the power plant being more than 5 MW, preferably more than 10 MW, more preferably more than 50 MW, particularly preferably more than 100 MW.
  • the power class can also be several 100 MW.
  • the heat of the carrier gas can be used to generate steam, to preheat feed water and/or to superheat steam.
  • the heat to the carrier gas in the form of hot air Feed combustion chamber of a (conventional) coal-fired power plant and/or a combined cycle power plant to burn a fuel such as coal or gas.
  • the power class of the coal-fired power plant and/or the combined cycle power plant can preferably correspond to the above-mentioned power class of a steam power plant.
  • the invention also allows the heat transferred to the carrier gas to be used in a gasification process to generate hydrogen.
  • the heat can be used to generate steam, which is then used in an allothermal coal gasification process.
  • thermoelectric storage power plant can have at least one compressor for compressing the carrier gas, at least one gas heater for heating the carrier gas, a plurality of heat storage modules for storing the heat from heated carrier gas and at least one heat exchanger, such as a steam generator, for transferring the heat from heated carrier gas to a Have working fluid of a steam power process.
  • the storage power plant according to the invention can also have other components of a steam power plant known from the prior art, such as a feed water pump, a condenser and a steam turbine.
  • the method according to the invention and the storage power plant according to the invention can make a contribution to load management in the power grid, with at times higher Power generation and low power demand during a loading cycle electrical energy is stored in the form of heat.
  • At peak loads at least one heat storage module is then discharged in a discharge cycle and the hot carrier gas thus generated is used to generate electricity, for example to evaporate water for a steam power process.
  • the electrical energy generated can be fed back into the power grid.
  • An operator of the storage power plant according to the invention can offer system services and participate in the control energy market.
  • the heat storage modules used make it possible to store electrical energy in the form of heat in a simple and cost-effective manner, with electrical power being used in the event of short-term high consumption peaks can be made available flexibly, in a very short time and at low cost.
  • a purely electrical heating of the carrier gas in at least one electrical air heater by converting electrical energy into thermal energy is particularly preferred. It is then not necessary to burn a fuel for the generation of hot carrier gas, so that an additional release of carbon dioxide is avoided.
  • a hot carrier gas can also be generated by burning at least one energy carrier in at least one combustion chamber of the gas heater, for example by burning biogas from biomass fermentation and/or synthesis gas from biomass gasification.
  • Using natural gas is also possible and an advantage.
  • energy can also be generated using other fossil fuels, such as synthesis gases from coal gasification.
  • Solid fuels can also be used.
  • the power plant according to the invention can thus contribute to covering the base load, for example in the vicinity of a biogas plant, which allows cost-effective generation of electricity.
  • the power plant according to the invention is characterized for isolated operation, with electricity being generated in a decentralized manner from fuels that are preferably generated from renewable sources.
  • waste or process heat from a secondary process is also used in the gas heater to generate hot gas.
  • a plurality of heat storage modules connected in series can form a heat storage row, with a carrier gas being heated in at least one gas heater to a specific loading target temperature and subsequently a plurality of heat storage modules of the heat storage row, in particular all heat storage modules, flows through.
  • the heat storage modules are thus heated or "loaded” to the same or different heat storage temperatures depending on the size of the hot gas volume flow, the level of the target loading temperature of the hot carrier gas when it exits the gas heater, the size of the respective heat storage module and/or the heat capacity of the heat storage material used ". All heat storage modules are preferably of the same design and have the same usable heat content in a fully loaded state.
  • heat storage modules are controlled at least in pairs.
  • the at least paired activation of heat storage modules simplifies the structural design of the heat storage modules and their interconnection with regard to the required pipe lengths and thus enables cost-effective production of the modules.
  • At least two heat storage modules are controlled together for charging, i.e. released for the flow of hot carrier gas for common charging in series connection.
  • At least two heat storage modules can form a heat storage pair.
  • Several pairs of heat accumulators of a heat accumulator system can be controlled independently of one another or separately. This can be achieved by appropriate piping and valve control in the heat storage system.
  • the heat accumulator modules of the respective pair of heat accumulators can be arranged in series and the carrier gas can then flow through them.
  • activation in pairs can be provided when discharging the heat storage modules.
  • each individual heat storage module can then be activated as required, i.e. can be released for a flow of carrier gas.
  • Hot carrier gas from a gas heater with a high, preferably a maximum, Occur loading setpoint temperature the hot carrier gas cools during loading of the first heat storage module and exits the heat storage module with a lower outlet temperature.
  • the carrier gas is then fed to the subsequent heat storage module of the heat storage row for charging.
  • the outlet temperature of the carrier gas flowing out of the respective heat storage module increases during a loading cycle.
  • the exit temperature of the carrier gas when exiting a preceding heat storage module preferably essentially corresponds to the entry temperature of the carrier gas when entering the following heat storage module.
  • the heat storage modules of a heat storage row preferably heat up to different degrees during a charging cycle, with the heat content of the heat storage modules that is reached during a charging cycle and that can be used during the discharge and, preferably, the heat storage temperature, gradually decreasing in the direction of flow of the carrier gas from heat storage module to heat storage module. Accordingly, the outlet temperature of the carrier gas decreases from heat storage module to heat storage module.
  • At least one last heat storage module of the heat storage row is not fully loaded in each loading cycle.
  • the carrier gas can then exit this heat storage module cold, ie at an exit temperature of, for example, less than 100° C., preferably less than 50° C., in particular less than 30° C.
  • the charging procedure described enables simple and cost-effective storage of electrical energy, with the heat contained in the carrier gas being largely completely stored in the heat storage modules and being made available again in the short term.
  • the carrier gas emerging from a heat storage module when it is being charged can be used to charge a subsequent heat storage module in the heat storage row until the outlet temperature of the carrier gas from the preceding heat storage module falls below a predetermined minimum outlet temperature.
  • the minimum outlet temperature can be less than 200°C, preferably less than 100°C, more preferably less than 50°C, particularly preferably less than 30°C. Is the minimum outlet temperature still sufficiently high, the carrier gas emerging from a heat storage module can be used for heat retention purposes, for example in the steam power process.
  • the loading of a subsequent heat storage module in the heat storage row can also be carried out at least partially by direct supply of hot carrier gas from a gas heater, in particular if the outlet temperature of the carrier gas from a preceding heat storage module in the heat storage row falls below a predetermined minimum outlet temperature.
  • the directly supplied hot carrier gas from the gas heater can have the desired loading temperature, which is reached at maximum in the gas heater, so that a preferably complete loading of a subsequent heat storage module is possible.
  • the subsequent heat storage module can be charged with the carrier gas from a preceding heat storage module in the heat storage row and by supplying hot Carrier gas done from the gas heater.
  • the direct supply of hot carrier gas thus makes it possible to achieve a certain high loading state of the subsequent heat storage module in a simple manner.
  • a plurality of heat storage modules can be loaded in parallel, with each heat storage module being supplied with a separate hot carrier gas stream.
  • a plurality of heat storage modules can preferably be activated at least in pairs.
  • at least two heat storage modules can form a heat storage unit or a heat storage pair.
  • a plurality of heat storage units can be charged in parallel, but the respective heat storage modules of a heat storage unit are connected in series and the carrier gas then flows through them.
  • the heat storage units can preferably be controlled independently of one another. A corresponding control can be provided for the discharge.
  • a plurality of gas heaters can be provided to generate separate carrier gas streams, with each heat storage module being assigned at least one gas heater can be.
  • a stream of carrier gas with a specific target loading temperature exits from each gas heater in order to load the associated heat storage module.
  • the target loading temperatures of the carrier gas streams can be the same or different. In all gas heaters, a maximum target loading temperature of between 1000° C. and 1300° C. is preferably achieved.
  • the parallel loading of several heat storage modules enables in particular a simultaneous high, preferably complete, loading of the heat storage modules in a very short time.
  • heat storage modules can be discharged in parallel to generate a heated carrier gas flow for the provision of heat in the power plant and/or gasification process, with each heat storage module being able to be supplied with a separate cold carrier gas flow.
  • a heat storage module with the comparatively lowest heat storage temperature and at least one heat storage module with a comparatively next higher heat storage temperature of a plurality of heat storage modules are discharged in parallel in order to provide a carrier gas flow with a desired target discharge temperature.
  • the heat storage modules are preferably discharged simultaneously.
  • at least two carrier gas streams of different temperatures are mixed in order to set or adjust a specific target discharge temperature of the carrier gas required for the subsequent heat transfer to the power plant and/or gasification process.
  • This target discharge temperature can be kept constant over the entire discharge cycle of the heat storage modules by suitable volume control of the combined carrier gas flows.
  • a loaded heat storage module with a lower heat content and / or with a lower heat storage temperature can thus be used in a discharge cycle as a bypass for a loaded heat storage module with a higher heat content and / or a higher heat storage temperature.
  • carrier gas heated during the discharge of at least one heat storage module can be combined with cold carrier gas, in particular with cold air, in order to cool the heated carrier gas to a specified target discharge temperature of the carrier gas. This allows easy and accurate regulation of the target discharge temperature of the carrier gas.
  • carrier gas heated in at least one heat storage module is mixed directly with hot carrier gas from the gas heater.
  • the carrier gas from the gas heater is preferably at the maximum load set point temperature.
  • the heat transferred to the carrier gas in a gas heater can also be used directly, without intermediate storage of the heat in a heat storage module, in a process for generating electricity and/or hydrogen.
  • part of the hot carrier gas generated in the gas heater is fed past the heat storage modules to at least one steam generator of the steam power process in order to keep the steam generator warm during a charging cycle of the heat storage modules.
  • At least one heat storage module is completely discharged and at least one heat storage module is only partially discharged during a discharge cycle.
  • the outlet temperature of the carrier gas from the heat storage module at the end of the discharge cycle is preferably less than 200° C., preferably less than 100° C., more preferably less than 50° C., particularly preferably less than 30° C.
  • heat storage modules with a higher heat content are preferably not completely discharged in a discharge cycle.
  • the heat storage module with the lowest heat content in particular with the lowest heat storage temperature, is first discharged and then heat storage modules with respectively increasing usable heat content and/or with respectively increasing heat storage temperature,
  • the hot carrier gas generated during a discharge cycle can be used to generate steam in a steam power process, whereby the electrical efficiency of the storage power plant can be increased by first expanding the heated carrier gas in an expander or a gas expansion turbine of the storage power plant and then feeding it to a steam generator.
  • the absolute pressure of the carrier gas before it enters the gas expansion turbine can be up to 20 bar. A corresponding compression of the cold carrier gas is provided for this purpose. If the electricity is only generated in the steam power process, an absolute pressure of the carrier gas between 2 and 5 bar, preferably between 3 and 4 bar, is sufficient, with which the heated carrier gas can be fed to a steam generator.
  • an upstream expander or gas expansion turbine can be provided in order to increase the electrical efficiency of the storage power plant.
  • the expander can be connected downstream of the heat storage modules and upstream of a steam generator in the flow direction of the carrier gas.
  • the carrier gas can be heated in at least one gas heater and then used directly, ie without loading and unloading the heat storage modules, to generate steam in the steam process.
  • the carrier gas is heated in the gas heater by burning a fossil fuel such as natural gas.
  • a fossil fuel such as natural gas.
  • non-fossil energy sources such as biogas is also possible.
  • indirect heating of the carrier gas can be provided in order not to contaminate the carrier gas with combustion gases.
  • the carrier gas can be circulated.
  • the carrier gas is not discharged to the environment after the heat has been transferred to the working fluid, but is used to reload the heat storage modules.
  • An essentially closed carrier gas system can then be present.
  • the carrier gas is discharged to the environment after heat transfer to the working fluid, an open carrier gas system is present, which requires the supply of fresh carrier gas for a subsequent loading cycle.
  • the Figures 1 to 4 show a thermoelectric storage power plant 1 for using the heat from heated carrier gas 2 to generate electricity, with a compressor 3 for compressing the carrier gas 2, with a plurality of gas heaters 4a-d for heating the carrier gas 2, with a plurality of heat storage modules 5a-d for Storing the heat from heated carrier gas 2 and having a steam generator 6 for transferring the heat from heated carrier gas 2 to a working fluid 7 of a steam power process.
  • the carrier gas 2 is preferably air or another suitable gas.
  • the working fluid 7 is preferably water.
  • Each gas heater 4a-d has a combustion chamber 8 for the use of gaseous energy carriers 8a, such as biogas or natural gas, and an electric heater 9, which has a heating conductor, for example made of silicon carbide or a suitable metal, and can be connected to a power source. When the power source is switched on, the heating conductors heat up and transfer their heat to the carrier gas 2 . With a suitable design of the gas heaters 4a-d, the carrier gas 2 can be heated to a target loading temperature of, for example, a maximum of 1200°C. The desired loading temperature is specified as a desired value for a control and/or regulating device (not shown).
  • the carrier gas 2 is first heated in at least one gas heater 4 to the desired charging temperature.
  • the volume regulation of the system is designed in such a way that, depending on the amount of electrical energy generated, the specified loading setpoint temperature for the carrier gas 2 at the exit from a gas heater 4a-d is maintained.
  • several gas heaters 4a-d can also be operated simultaneously, a partial flow of the carrier gas 2 being fed to a gas heater 4a-d via a gas line 10a-d and heated there.
  • the partial flows can be brought together via a collecting line 11 and fed to a first heat storage module 5a in order to thermally load the heat storage module 5a by releasing heat from the heated carrier gas 2 to a heat storage material of the heat storage module 5a.
  • a feed valve 12a is open, while other feed valves 12b-d, which connect the other heat storage modules 5b-d to the associated gas heaters 4b-d, are closed.
  • the heat storage modules 5a-d are connected in series and form a heat storage row, with the carrier gas 2 heated to the charging setpoint temperature in the gas heater 4a subsequently flowing through the heat storage modules 5b-d of the heat storage row and the heat storage modules 5a-d during a charging cycle be heated.
  • the carrier gas 2 initially leaves the heat storage module 5a cold via a three-way valve 13a. As the heat absorption of the storage mass increases, the temperature of the carrier gas 2 flowing out of the heat storage module 5a increases.
  • the three-way valve 13a has two switching options.
  • the carrier gas 2 can be fed to a chimney 17 as exhaust air either via the collecting line 14 , the outlet valve 15 and a heat exchanger 16 .
  • the carrier gas 2 is supplied to the subsequent heat storage modules 5b-d via the three-way valves 13a-c if there is sufficient heat content or if the heat storage temperature is sufficient. This takes place via the supply lines 18a-c.
  • the heat energy contained in the carrier gas 2 can be largely completely stored in the heat storage modules 5a-d.
  • the heat storage module 5b is preferably designed in such a way that cold carrier gas 2 also exits from the heat storage module 5b when the heat storage module 5a is fully loaded. There is complete loading when the outlet temperature of the carrier gas 2 from the heat storage module 5a corresponds to the inlet or loading target temperature of 1200° C., for example.
  • the carrier gas 2 leaving the heat storage module 5a is fed to the third heat storage module 5c via the three-way valve 13b and the feed line 18b.
  • the carrier gas 2 can be discharged to the environment via the collecting line 14 . It is possible to also load the heat storage module 5d or to switch on other heat storage modules that are not shown.
  • the gas heaters 4a-d can each supply the individual heat storage modules 5a-d with heated carrier gas 2, which is possible via the charging lines 19a-d and, if necessary, other valves that are not shown.
  • a heat storage module 5b-d can also be fully charged if the heat content of the carrier gas 2 emerging from the previous heat storage module 5a-c is not sufficient for a complete charging of the subsequent heat storage module 5b-d.
  • the hot carrier gas streams generated in the gas heaters 4a-d are brought together via the collecting line 11 and that the heat storage modules 5a-d are subsequently flowed through, starting from the first heat storage module 5a for a loading of hot gas.
  • a partial flow of the hot carrier gas 2 from the collecting line 11 is mixed with a partial flow of cold carrier gas 2, which is supplied via the compressor 3, and can be supplied to the steam generator 6 to keep it warm.
  • the temperature can be controlled via the size of the volume flows.
  • the heat storage modules 5a-d can be thermally insulated vessels in which a heat-storing mass, for example a pebble bed made of ceramic material, is arranged. Suitable heat storage materials are known to those skilled in the art.
  • the heat storage mass is heated by the hot carrier gas 2 while the carrier gas 2 cools down.
  • the efficiency in the conversion electrical power in heat and transfer of heat to the storage mass more than 90%, preferably more than 95%.
  • carrier gas 2 is supplied via an open supply valve 20 to the compressor 3, with which carrier gas 2 can be supplied to the gas heaters 4a-d via a preheater 21 and a collecting line 22 as well as further supply valves 23a-d. According to 1 the entire carrier gas 2 is only supplied to the first gas heater 4a when the inlet valve 23a is open. The supply valves 23b-d are closed. In principle, however, as described above, heating of the carrier gas 2 can also be provided in several or all gas heaters 4a-d.
  • the supply valves 23a-d are closed. Instead, further inlet valves 24a-d are opened, so that cold carrier gas 2 is pressed into the heat storage modules 5a-d via the compressor 3 and the collecting line 22 for parallel discharge of the heat storage modules 5a-d.
  • the carrier gas 2 is heated in the heat storage modules 5a-d.
  • the carrier gas 2 can be routed in parallel over all heat storage modules 5a-d, or it is possible to only discharge one or more heat storage modules 5a-d.
  • the carrier gas 2 can be brought together in a further collecting line 25.
  • the collecting line 25 is connected to the heat storage modules 5a-d via outlet lines 26a-d.
  • the carrier gas 2 emerges from the heat storage modules 5a-d at the maximum loading setpoint temperature of 1200°C.
  • preheated carrier gas 2 can be fed at least partially past the heat storage modules 5a-d into the collecting line 25 via bypass lines 27a-d.
  • This makes it possible to mix hot carrier gas from the heat storage modules 5a-d and cold carrier gas 2 via a corresponding volume control in such a way that a desired discharge target temperature of the hot carrier gas 2 is set.
  • This desired discharge temperature can be between 600° C. and 800° C., for example. This temperature is preferably kept constant over the entire discharge operation. Is the exit temperature when the carrier gas exits 2 from a heat storage module 5a-d is greater than the desired target discharge temperature, the temperature can be regulated via the respective bypass lines 27a-d.
  • the heat storage modules 5a-d are arranged in a heat storage row, it can be provided that the heat storage modules 5a-d are emptied depending on the usable heat content and/or the heat storage temperature of the respective heat storage module 5a-d, starting with a heat storage module 5d that has the lowest heat content and/or can have the lowest heat storage temperature, subsequently the heat storage modules 5c, 5b, 5a, i.e. in the opposite direction to the loading, are discharged.
  • the discharge thus preferably begins with the heat storage module that has the lowest usable heat content and/or the lowest heat storage temperature.
  • the respective heat storage module is discharged, which in turn has the lowest usable heat content or the lowest heat storage temperature in comparison to the remaining heat storage modules.
  • not all heat storage modules 5a-d have to be completely discharged. With the method described, a high system efficiency can be achieved and the electrical power generated can be adapted to the actual requirement.
  • the outlet temperature of the carrier gas 2 from the last heat storage module 5d in the heat storage row falls below a predetermined target discharge temperature
  • a partial flow of the carrier gas 2 is passed over the preceding heat storage 5c in the heat storage row with a higher heat content and/or a higher heat storage temperature.
  • the carrier gas streams are brought together so that the target discharge temperature is set.
  • the heat storage module 5d then serves as a bypass, which is operated until the heat storage module 5d is completely empty.
  • the desired discharge setpoint temperature of the carrier gas 2 is achieved by discharging at least one upstream heat storage module 5a to 5c of the heat storage row, with the temperature being able to be regulated again if necessary by supplying cold carrier gas 2 via at least one bypass line 27a-d.
  • the compressor 3 preferably compresses the carrier gas 2 to a system pressure of up to 20 bar.
  • the hot carrier gas produced during a discharge cycle 2 is fed to an expander 28 via the collecting line 25 and expanded in the expander 28 .
  • the carrier gas 2 cools down depending on the pressure level. If the use of an expander is not intended, the system pressure can be significantly lower and, for example, only be between 3 and 4 bar (absolute).
  • the carrier gas 2 emerging from the expander 28 serves to generate and superheat high-pressure steam in the steam generator 6.
  • the steam generator 6 can have a preheater 29, a steam drum 30 and a superheater 31. Otherwise, the steam generator 6 corresponds to a conventional design.
  • the generated steam is supplied to a steam turbine 32 .
  • the expander 28 and the steam turbine 32 are connected to a generator, not shown. Incidentally, a degasser 33 and a condenser 34 can be provided.
  • the electrical efficiency of the storage power plant 1 can reach up to 60%. In addition, it is possible to decouple district heating. The thermal efficiency when using district heating can reach up to 98%. Process steam can also be extracted from the storage power plant 1 .
  • FIGS Figures 3 and 4 show operation of the storage power plant 1 with an open carrier gas system, with the carrier gas 2 being discharged to the environment as exhaust air via the chimney 17, there is the possibility of circulating the carrier gas 2.
  • FIGS Figures 3 and 4 show where 3 the state during a loading cycle and 4 shows the state during a discharge cycle.
  • the carrier gas system When the carrier gas system is closed, a supply of fuel gas and the combustion of the fuel gas in the combustion chambers 8 of the gas heaters 4a-d are preferably not provided, but this is possible with indirect heat transfer. Instead, the carrier gas 2 is preferably heated exclusively by means of heating conductors by converting electrical energy into thermal energy. If the carrier gas 2 is circulated, the outlet valve 15 is closed when the heat exchanger modules 5a-d are loaded. Instead, the circuit valves 35 , 36 are open, so that carrier gas emerging from a heat storage module 5 a to 5 d is supplied to the compressor 3 via the collecting line 14 and a circuit line 37 . The inlet valve 20 is closed, so that no fresh carrier gas 2 is fed into the carrier gas system.
  • the carrier gas 2 is returned via a return line after passing through the preheater 21 38, an open recirculation valve 39 and the circuit line 37 fed to the compressor and is then available for renewed loading of the heat storage modules 5a-d Allows carrier gas system via an outlet line 41 and the chimney 17 ( 2 ), are closed.
  • a further combustion chamber 42 can be provided as part of a further gas heater, with which it is possible to bring the carrier gas 2 to a specific target temperature of, for example, 600° C. to 800° C. before it enters the expander 28 by burning fuel gas 8a heat.
  • the gas heater can be designed for direct or indirect heat transfer. This enables the storage power plant 1 to be used to cover the base load, with loading and unloading of the heat storage modules 5a-d not being necessary for this.
  • the combustion chamber 42 can also be used to provide hot gas for keeping machines warm when the heat storage modules 5a-d are loaded. The heating of the carrier gas in the combustion chamber 42 can also contribute to reducing the electricity production costs.
  • FIG. 5 to 8 a wiring example for the charging and discharging of four heat storage modules 5a-d is shown schematically.
  • figure 5 and 6 show the interconnection when loading the heat storage modules 5a-d, while 7 and 8 show the interconnection when discharging the heat storage modules 5a-d.
  • carrier gas 2 is heated in a gas heater 4a, which is designed as an air heater, and according to figure 5 then fed to the heat storage modules 5a-d.
  • the carrier gas 2 can be air.
  • the hot carrier gas 2 from the gas heater 4a flows through the series-connected heat storage modules 5a-d below.
  • the heat storage modules 5a-d can be controlled in pairs or carrier gas 2 can flow through them. This applies equally to loading and unloading.
  • the first two heat storage modules 5a and 5b shown on the left and the further heat storage modules 5c and 5d shown on the right each have a heat storage pair or assigned to a heat accumulator unit, the heat accumulator pairs being controlled separately and independently of one another due to the routing of the lines, and carrier gas 2 being able to flow through them. It goes without saying that more than two heat storage modules 5a-d can also be assigned to a separately controllable heat storage pair if the storage arrangement comprises more than four heat storage modules 5a-d.
  • each with two heat accumulator modules 5a, 5b or 5c, 5d are connected in series and the hot carrier gas 2 from the gas heater 4a flows through them in succession.
  • the carrier gas 2 is here according to figure 5 circulated via a circulatory line 50 and, after exiting from the in figure 5 fourth heat storage module 5d shown on the right via a compressor 3 back to the gas heater 4a.
  • the gas flow is achieved through appropriate control of a plurality of valves.
  • the four heat storage modules 5a-d can also be loaded in such a way that hot carrier gas 2 from the gas heater 4a flows through the two heat storage pairs with the heat storage modules 5a, 5b on the one hand and 5c, 5d on the other hand in parallel.
  • the carrier gas 2 exits the gas heater 4a at a specific loading target temperature and is supplied at this temperature to the respective first heat storage module 5a or 5c of the respective heat storage pair. This allows full loading.
  • the hot carrier gas 2 from the gas heater 4a is routed past the two heat storage modules 5a, 5b of the first heat storage pair via a bypass line 43 and thus reaches the heat storage module 5c of the in 6 heat accumulator pair shown on the right. It is also possible to feed hot carrier gas 2 from the gas heater 4a directly to a consumer 45 via a consumer line 44, with the term "consumer" in the context of the invention encompassing any possible use of the heat from the hot carrier gas 2 in a power plant process and/or gasification process.
  • the wiring according to 6 to supply fresh air 46 via a further compressor 47 and a control line 52 to a mixing chamber 48 in order to regulate the temperature of the hot carrier gas 2 accordingly before it is passed on to the consumer 45 .
  • the fresh air 46 is on one significantly lower temperature level than the hot carrier gas 2 emerging from the gas heater 4a.
  • fresh air 46 which forms the carrier gas 2
  • the fresh air 46 or the carrier gas 2 then flows through the two heat storage modules 5a, 5b of the in 7 pair of heat accumulators shown on the left and reaches the consumer 45 via the bypass line 43 and the consumer line 44.
  • fresh air 46 can be supplied to the carrier gas 2 via the control line 52 and the mixing chamber 48 in order to achieve a specific useful temperature of the carrier gas 2 for the Set or regulate power plant process and / or gasification process.
  • According to 8 can fresh air 46 via the compressor 47, 3 and a discharge line 51 to the last heat storage module 5d of the in 8 heat accumulator pair shown on the right.
  • the carrier gas 2 heated in the heat storage modules 5c, 5d reaches the mixing chamber 48 via the bypass line 43.
  • fresh air 46 is fed via the bypass line 49 to the heat storage modules 5a, 5b of the other heat storage pair and heated there.
  • the carrier gas 2 heated in the heat storage modules 5a, 5b also reaches the mixing chamber 48 via the bypass line 43.
  • the two heat storage pairs are thus discharged in parallel, while the heat storage modules 5a, 5b or 5c, 5d of each heat storage pair are discharged in series.
  • the temperature of the heated carrier gas 2 can be regulated as required by supplying fresh air 46 via the control line 52 to the mixing chamber 48 .
  • the carrier gas 2 then reaches the consumer 45.
  • a direct Supply of hot carrier gas 2 from the gas heater 4a into the mixing chamber 48 is possible in order to increase the temperature of the carrier gas 2 heated in the heat storage modules 5a-d.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Fuel Cell (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP15790029.1A 2014-10-17 2015-10-16 Verfahren zum ausgleich von lastspitzen bei der energieerzeugung und/oder zur erzeugung von elektrischer energie und/oder zur wasserstofferzeugung Active EP3207225B1 (de)

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DE102014015323 2014-10-17
DE102014017346.1A DE102014017346A1 (de) 2014-10-17 2014-11-25 Verfahren und Speicherkraftwerk zum Ausgleich von Lastspitzen bei der Energieerzeugung und/oder zur Erzeugung von elektrischer Energie
PCT/EP2015/002050 WO2016058701A1 (de) 2014-10-17 2015-10-16 Verfahren zum ausgleich von lastspitzen bei der energieerzeugung und/oder zur erzeugung von elektrischer energie und/oder zur wasserstofferzeugung sowie speicherkraftwerk

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PL3269948T3 (pl) 2016-07-15 2022-07-18 Carbon-Clean Technologies Gmbh Sposób dostosowania mocy elektrowni z turbiną parową i elektrownia z turbiną parową
AT520477B1 (de) * 2017-09-15 2019-10-15 Franz Matthias Schweighofer Vorrichtung zum Erzeugen von Dampf
US11236950B2 (en) 2018-04-18 2022-02-01 Carbon-Clean Technologies Gmbh Method for operating a regenerative heat storage arrangement and heat storage arrangement
CN109945268B (zh) * 2019-01-28 2020-08-07 太原理工大学 一种燃气-蒸汽联合循环热电厂的供热系统
KR102384981B1 (ko) * 2020-05-15 2022-04-08 한국지역난방공사 열변환장치를 활용한 가상발전소 시스템 및 이를 이용한 가상발전소 운영 방법
CN114383185B (zh) * 2020-10-19 2023-05-02 辽宁省鑫源温控技术有限公司 利用峰谷电价差异节约采暖费用的方法、存储介质和温控器
CN112344413B (zh) * 2020-10-30 2022-07-15 广西电网有限责任公司电力科学研究院 一种热电联产机组低压汽源升压供热方法

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4161211A (en) 1975-06-30 1979-07-17 International Harvester Company Methods of and apparatus for energy storage and utilization
US4003786A (en) * 1975-09-16 1977-01-18 Exxon Research And Engineering Company Thermal energy storage and utilization system
US4089744A (en) * 1976-11-03 1978-05-16 Exxon Research & Engineering Co. Thermal energy storage by means of reversible heat pumping
DE7828904U1 (de) * 1978-09-28 1980-02-14 Maschinenfabrik Augsburg-Nuernberg Ag, 8000 Muenchen Waermespeichereinrichtung fuer thermische energieerzeugungsanlagen
US4362149A (en) * 1980-12-08 1982-12-07 Rockwell International Corporation Heat storage system and method
CH659855A5 (de) * 1981-11-16 1987-02-27 Bbc Brown Boveri & Cie Luftspeicher-kraftwerk.
DE3931582A1 (de) 1989-09-22 1991-04-04 Krantz Gmbh Energieplanung H Verfahren zur nutzung von hochtemperaturabwaerme
JP3646630B2 (ja) * 2000-07-27 2005-05-11 株式会社日立製作所 蓄熱・蓄冷槽
JP2003056841A (ja) * 2001-08-10 2003-02-26 Chugai Ro Co Ltd 燃焼排ガスの顕熱回収方法
DE102004050465B3 (de) * 2004-09-28 2005-09-15 Applikations- Und Technikzentrum Für Energieverfahrens-, Umwelt- Und Strömungstechnik (Atz-Evus) Verfahren zur Erwärmung und/oder Verdampfung eines Fluids
US7444818B1 (en) 2005-11-23 2008-11-04 Florida Turbine Technologies, Inc. Batch fired heat reservoirs
DE102009038323A1 (de) * 2009-08-21 2011-02-24 Krones Ag Verfahren und Vorrichtung zur Verwertung von Biomasse
GB201104867D0 (en) * 2011-03-23 2011-05-04 Isentropic Ltd Improved thermal storage system
EP2594753A1 (en) * 2011-11-21 2013-05-22 Siemens Aktiengesellschaft Thermal energy storage and recovery system comprising a storage arrangement and a charging/discharging arrangement being connected via a heat exchanger
DE102011088380A1 (de) * 2011-12-13 2013-06-13 Siemens Aktiengesellschaft Energiespeichervorrichtung mit offenem Ladekreislauf zur Speicherung saisonal anfallender elektrischer Überschussenergie
EP2698505A1 (de) 2012-08-14 2014-02-19 Siemens Aktiengesellschaft Verfahren zum Laden und Entladen eines Wärmespeichers und Anlage zur Speicherung und Abgabe von thermischer Energie, geeignet für dieses Verfahren
WO2014052927A1 (en) * 2012-09-27 2014-04-03 Gigawatt Day Storage Systems, Inc. Systems and methods for energy storage and retrieval
DE102013008445B4 (de) * 2013-05-20 2022-12-29 Witt Solar Ag Wärmespeicherkraftwerk
US20150113940A1 (en) * 2013-10-25 2015-04-30 Mada Energie Ltd Systems, methods, and devices for liquid air energy storage in conjunction with power generating cycles

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CA2964850A1 (en) 2016-04-21
JP2017537269A (ja) 2017-12-14
PL3207225T3 (pl) 2023-03-06
EP3207225A1 (de) 2017-08-23
PT3207225T (pt) 2022-12-14
DE102014017346A1 (de) 2016-04-21
ES2935725T3 (es) 2023-03-09
US10309258B2 (en) 2019-06-04
DK3207225T3 (da) 2022-12-19
CA2964850C (en) 2019-06-25
US20170241296A1 (en) 2017-08-24
CN107429576B (zh) 2020-01-14
CN107429576A (zh) 2017-12-01
WO2016058701A1 (de) 2016-04-21

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